Apparatus for making shrinkable tubing

ABSTRACT

Long lengths of a heat-shrinkable sleeve for use in splicing electrical cables and the like are made in a continuous process. The sleeve is formed around a permeable core, and the core and sleeve are advanced together in an axial direction, the leading end of the advancing sleeve being hermetically sealed. The core and sleeve pass through a heating station, thereby heating a portion of at least the sleeve, and a fluid is introduced under pressure into the core, thereby internally pressurizing the sleeve to effect a radial expansion of the heated portion thereof. The core and sleeve then pass through a cooling station, thereby cooling the expanded sleeve to stabilize it. A stress graded compound also for use in splicing electrical cables and the like is made by heating a dimethyl silicone liquid to remove entrapped gas and mixing the liquid with a silicone carbide powder having a particle size capable of passing through a 400 mesh screen. The volumetric proportion of powder to 1 part liquid is within the range of 0.5 part to 2.0 parts.

This is a division of application Ser. No. 410,443, filed Aug. 23, 1982,now U.S. Pat. No. 4,446,095.

BACKGROUND OF THE INVENTION

The present invention relates to the splicing or joining of electricalcables and, more particularly, to a novel, continuous method ofmanufacture of a shrinkable composite sleeve used in forming a splice orjoint, to apparatus for practicing the method, to a novel, highlyeffective stress control material compatible with the semiconductivecomponents of the sleeve and of the cable for which the splice or jointis provided, and to a method of manufacturing the stress controlmaterial.

A copending U.S. patent application of George Bahder Ser. No. 319,429,filed Nov. 9, 1981, and assigned to the assignee of the presentinvention, discloses a new type of splice or joint especially adaptedfor splicing high-voltage power cables. The joint comprises ashrinkable, composite sleeve and high-resistive stress controlcomponents of which one is an integral part of the composite sleeve andthe other is a separate layer of high electrical resistivity andmechanically resilient characteristics.

Said patent application Ser. No. 319,429 discloses a method of producingthe shrinkable sleeve in a sequence of separate operations.Specifically, the three-layer polymeric composite sleeve is manufacturedin one or more extrusion and curing passes over a metallic core. In asubsequent, completely separate process, the previously hardened sleeveis chopped into small lengths which then are placed into separatecylindrical containers. One of the ends of the sleeve is sealed,internal pressure is applied by introducing a pressurized fluid throughthe other end, and the sleeve is heated in a temperature sufficient toallow for the softening and expansion of the sleeve. Subsequently, theexpanded sleeve is cooled to room temperature. Since the ends of eachsleeve have to maintain their original dimensions, in order not toloosen the seals, the sections of sleeve being set up for expansion haveto be significantly longer than the useful length of the sleeves.Subsequently, a significant part of the total length is discarded, sinceonly the part having uniform expanded dimensions is useful.

The nonuniform expansion along the length of sleeve requires carefulcontrol of the process. In particular, the timing for pressureapplication during the heating step becomes critical, in order tominimize cracks and voids.

SUMMARY OF THE INVENTION

One object of the present invention is to provide a method ofmanufacturing long lengths of a heat-shrinkable sleeve for use insplicing electrical cables and the like, wherein no danger of voidsand/or cracks forming in the body of the sleeve exists. In particular,an object of the invention is to provide a process which enables themanufacture of a three-layer expanded sleeve in one continuousoperation, which reduces substantially the overall effort required, andwhich ensures the high quality of the expanded composite sleeve withpractically no waste.

Another object of the invention is to provide an improved mixture formanufacturing a stress graded compound for splicing electrical cablesand the like and a method of manufacturing the compound.

The foregoing and other objects are attained in accordance with thepresent invention by a process with a number of significantcharacteristics:

(a) Long lengths of a multi-layer composite sleeve are manufactured andapplied over a core that allows for internal fluid pressure application.This manufacture employs an insulating material having thermosetcharacteristics resulting from crosslinking.

(b) The leading end of the sleeve is hermetically sealed, and fluidpressurizing means is attached to the other end of the length (which maybe thousands or tens of thousands of feet away).

(c) The composite unexpanded sleeve is fed to the expansion system bymeans of a constant speed supply device.

(d) The metallic part of the inner core is rapidly heated by induction,and immediately afterward or simultaneously heat energy is supplied tothe insulation system by passing the sleeve through a specially sized,relatively long heating pipe.

(e) The sleeve is expanded by internal pressure in a conical section ofthe heating pipe.

(f) The expanded sleeve is cooled in two steps, the first in anexternally cooled pipe and the second under pressurized water, with apressure which is less than the expansion pressure.

(g) The expanded sleeve is dried and wound up in a continuous length ona drum.

(h) The metallic conductor is removed from the sleeve and cut intolengths suitable for joining of power cables.

Manufacture of the stress graded compound comprises the steps of heatinga dimethyl silicone liquid to remove entrapped gas and mixing the liquidwith a silicone carbide powder having a particle size capable of passingthrough a 400 mesh screen, the proportion of powder to 1 part liquid byvolume being within the range of 0.5 part to 2.0 parts. Preferablysubstantially 1 part powder to 1 part liquid by volume is employed. Theheating can be done in an evacuated environment or in air. If it is donein air, then fumed silica is preferably added to the mixture in anamount sufficient to increase the viscosity of the mixture to asatisfactory value.

BRIEF DESCRIPTION OF THE DRAWING

A better understanding of the invention may be gained from aconsideration of the following detailed description of the preferredembodiments thereof, in conjunction with the appended figures of thedrawing, wherein:

FIG. 1 is a view in end elevation, partly in section, of a pay-off orprocessing reel for supplying a long length of a sleeve in a firstcontinuous process according to the invention;

FIG. 2 is a view in axial section of a sleeve connected to means forpressurizing it internally in accordance with the invention;

FIG. 3 is a diagrammatic representation of the apparatus of FIGS. 1 and2 plus additional apparatus for carrying out the method of theinvention;

FIG. 4 is an enlarged view in axial section of a type of elastomericseal useful in the apparatus of FIGS. 3 and 5; and

FIG. 5 is a diagrammatic representation of apparatus for carrying out amethod according to the invention which is alternative to that describedbelow in connection with FIG. 3.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

The initial manufacture of a multi-layered sleeve such as 10 (FIGS. 1-3,where sleeve is shown as a single layer, for convenience) over astranded conductor is a standard procedure, similar to that used in themanufacture of high voltage cables, wherein a polymeric conductor shieldis applied over a metallic core, a relatively heavy layer of insulationis applied over the polymeric conductor shield, and over all aninsulation shield is applied. However, in the case of the sleeve 10 itis a requirement that the internal surface be as smooth as possible, anda binder is therefore applied over the stranded conductor, as forexample, one or more layers of tape. These tapes can be, for example,synthetic films such as polyethylene terephthalate. In addition, thecharacteristics of the inner shield are quite different from those ofthe conductor shield of a cable.

The inner layer of the sleeve 10 should normally have high resistivityor have a relatively high dielectric constant as compared to thedielectric constant of the cable insulation. For example, a dielectricconstant above 5 is suitable. It also should be of thermoset nature. Theinsulation of the sleeve 10 can be any of a variety of thermosetdielectrics used in the manufacture of cables.

This insulating material may be selected in accordance with the ultimateapplication of the sleeve in joining cables of different types. Forexample, it may be beneficial in some situations to use the sameinsulating material in the joint as in the cable. Materials such ascrosslinked polyethylene, ethylene propylene rubber or other thermosetinsulations are suitable. Finally, the insulation shield should also beof a thermoset nature, and it should have semiconducting qualitiessimilar to those used in the insulation shielding of cables.

The use of a stranded conductor or radially perforated thin tube isdesirable since internal pressure has to be applied to the inner surfaceof the three-layer composite sleeve 10 in order to achieve itsexpansion. This pressure may be lower than 30 atmospheres.

The above-described, non-expanded composite sleeve 10 is put up on apay-off or processing reel 12 provided with a side opening 14, asillustrated in FIG. 1. The inner end 16 of the sleeve 10 is pushedthrough this opening 14. The reel 12 to be used in the processing ofthese sleeves 10 is provided with means 10 to support a container 20 ofpressurized fluid, such as pressurized dry air, nitrogen or any othersuitable fluid. Alternatively, a compressor can be employed. The fluidcontainer 20 is provided with pressure regulating means 22.

The end 16 of the sleeve 10 (innermost part on the reel 12) is providedwith suitable connecting means 24 to apply pressure (as illustrated inFIG. 2) to the inner part 26 of the sleeve 10. The connecting means 24comprises a pipe 27 of which one end 28 is inserted within the sleeve 10and the other end 30 is inserted within a tube 32 connected through thepressure regulator 22 to the fluid supply 20. A clamp 34 ensures a tightfit between the tube 10 and the pipe 27. The pressurized fluid container20 rotates together with the reel 12.

FIG. 3 illustrates the equipment used in a first manufacturing processaccording to the invention. The sleeve 10 is supplied from the pay-offreel 12 to the heating-expansion-cooling section 36 of the processequipment by means of a control speed device 38 known in cablemanufacturing as a metering capstan. The capstan 38 includes opposedtreads 39a and 39b. The sleeve 10 passes through an induction heatingdevice 40 located between the metering capstan 38 and a lubricant sealbox 42. This induction heating device 40 comprises an AC power supply 42and a coil 44 electrically in series therewith and makes it possible tobring up rapidly the temperature of the metallic conductor 46 (FIG. 2)within the sleeve 10 by electromagnetic energy. The energy induced inthe conductor 46 is controlled so as not to exceed the temperature atwhich the thermoset insulation system is degraded. Temperatures shouldnormally be kept below 300° C.

Thereafter the composite sleeve 10 enters into a further heating section48 of the system. This heating section 48 is provided with the followingcomponents in the direction of the sleeve movement:

(a) the lubricant seal box 42

(b) a lubricant seal device 50

(c) a lubricant supply entry 52

(d) an electrical heating clamp 54

(e) a heating tube 56

The heating tube 56 extends from the inside of the lubricant sealing box42 and continues to a cooling pipe or tube 58. The heating tube 56includes immediately upstream of its downstream end a conical, or moreproperly a frusto-conical, expanding or expansion section 60.

Shortly downstream of the end of this conical expanding section is thecooling pipe 58. The first part 62 of the cooling pipe 58 has a coolingmantle 64. This is followed by a second cooling section 66, wherecooling liquid is applied directly to the expanded sleeve. Theelectrical AC heating circuit 68 heats only the tube 56 and terminatesupstream of the cooling section 58. In FIG. 3 it terminates immediatelybefore the cooling section, but it may also terminate prior to theexpansion section 60. The lubricant circulating system of which theupstream end (with respect to the movement of the sleeve 10) is in thelubricant seal box 42 may terminate downstream in the first section 62of the cooling tube 58. In FIG. 3 a lubricant exit system 70 is providedat the flanges 72, 73 joining the heating tube 56 and the first section62 of the cooling pipe 58.

A lubricant seal 74 is provided at the end of the first cooling section62. The pressurized cooling pipe 66 terminates in a water seal 76located inside a water seal box 78. The cooling system incorporates apressurized water circulating system including a pump 80, a heatexchanger 82 and a storage tank 84. Downstream of the water seal box 78the expanded sleeve 10 (not drawn to scale) proceeds into a dryingsection 86 and through a pull-out capstan device 88 from where itcontinues to a sleeve take-up 90. The equipment utilized downstream ofthe pressurized cooling pipe 66 is standard power cable manufacturingequipment.

The heating-expanding section 56, 60 and first section 62 of the coolingpipe are integral parts of one continuous pipe system. In the section56, the sleeve is allowed to expand to the diameter of the pipe, whichis calculated to have at least a diameter equivalent to the diameter ofthe sleeve without internal pressure, but expanded to a larger thanoriginal diameter in accordance with the coefficient of thermalexpansion of the sleeve insulation system; for example, in the case ofcross-linked polyethylene (XLPE) this radial expansion may be up to 15%of the diameter of the sleeve prior to entering the induction heatingcoil 44. The maximum diameter depends on the insulation system thicknessand the maximum temperature the sleeve 10 is subjected to. The diameterat the end of the expansion section 60 of the pipe is calculated inaccordance with the following formulae:

    Z=[(D.sup.2 -d.sup.2)K+(AK).sup.2 ].sup.1/2 +2δ      (1)

    K=(t.sub.m -t.sub.o)k                                      (2)

where:

Z=Inside diameter of the pipe 60 at the end of the expansion section

D=Outside diameter of the unexpanded sleeve 10 at room temperature

D=Inside diameter of the unexpanded sleeve 10 at room temperature

A=Largest diameter at room temperature over which the sleeve 10 has tofit plus clearance for eccentricity and

δ=Thickness of lubricant film

k=Coefficient of volumetric expansion per °C. of the polymer used in theinsulation system

t_(m) =Maximum temperature in °C. to be achieved in the heating pipe and

t_(o) =Room temperature

As mentioned, the expansion section 60 is followed immediately by acylindrical section 62 provided with a cooling mantle 64. At thedownstream end of the cooling mantle 64, a flange 92 is provided whichfacilitates attachment of the mantle 64 to a flange 94 of thepressurized cooling pipe 66. The seal 74 minimizes the entrance oflubricant into the pressurized cooling section 66.

The lubricating liquid in the heating-expanding section 56, 60 and firstsection 62 of the cooling pipe provides simultaneously a means tolubricate the sleeve 10 and facilitate its movement through the systemand to transfer heating energy into and from the sleeve 10. Thelubricant circulating system comprises a lubricant reservoir 98 providedwith heaters to bring the temperature of the lubricant to the maximumtemperature the sleeve will be exposed to. The system includes pumping,pressurizing and flow control equipment 100. The lubricant is introducedinto the heating pipe at the same end as the sleeve through a circularentrance 52. It is removed from the heating-expansion pipe 56, 60 by thecircular exit 70 located close to the end of the expansion section 60.From here the lubricant moves by gravity (FIG. 3 is diagrammatic) to acollecting reservoir 104 from where it is pumped back into the supplyreservoir 98. The whole lubricating system is closed.

Lubricants suitable for this operation are of the high molecular type,for example polyalkylene glycol such as UCON HB-5100, or dimethylsilicone fluids or polyhydroxy alcohol such as glycerol, entectic saltsor other liquids of similar characteristics, providing simultaneouslyhigh molecular weight, good high temperature heat transfer and goodlubricating characteristics. The high molecular weight characteristic isrequired in this operation to prevent the penetration of the liquid intothe mass of the composite sleeve 10 and especially into thesemiconducting layer, where it could affect adversely the electricalconducting characteristics of this layer.

The pressurized lubricant in the heating-expansion tube 56, 60 isprevented from exiting easily from this tube by means of seals.Elastomeric seals such as the one illustrated in FIG. 4 are suitable forthis purpose; also labyrinth or other types of seals can be used. InFIG. 4 the elastomeric seal is formed by a sleeve 106 extending beyond acylindrical, conical metallic pipe 108 and is held in place by acircular clamping device 110. The external pressure exerted by a fluidmedium on the seal provides the required sealing pressure. The supportpipe 108 and the seal are dimensioned so as to allow a close toleranceto the diameter of the cylindrical object passing through it. Theflexible part 107 of the seal 106 extending beyond the conical end 111has to be of longitudinal dimensions such that the radial force exertedon it is less than the longitudinal pulling force. In the case of theseal 74 (FIG. 3) installed at the exit end of the mantle 64 the requiredpressure to hold the lubricant inside the first section 62 of thecooling pipe is provided by the pressure of the cooling water within thepipe section 66.

The electric system for the heating of the composite sleeve passingthrough the pipe 56, 60 is provided by an A.C. power supply 112. Thecurrent to be supplied must be of such magnitude as to enable heating ofthe pipe to a maximum temperature of about 400° C., which issubstantially above the softening temperature of the composite sleeve tobe expanded in the system. For example, XLPE softens sufficiently forexpansion at about 120° C. The temperature to be used may vary dependingon the insulation used in the composite sleeve to be expanded. A.C.current is preferred for this heating system because it is the mosteffective, taking advantage of the skin effect of the pipe. The skineffect concentrates a higher density of current in the outermost part ofthe pipe, resulting in a higher and faster temperature rise. D.C.current or other means for heating these pipes such as heating mantles,resistor, heaters, etc., can also be used.

It is important that the heating energy be transmitted effectively,rapidly and uniformly into the sleeve to be expanded. The length of theheating section is calculated in accordance with the characteristics ofthe sleeve to be expanded. Factors to be considered are the speed withwhich the sleeve is pulled through the heating pipe, the wall thicknessof the sleeve insulating system, the dimension of the supporting coreand the efficiency of the heat transfer medium. The expansion section 60of the pipe is located at a sufficient distance from the entrance toallow the entire wall to reach the minimum softening temperature.Typical lengths are 50 ft. (about 15 meters) for the heating section 56,2 ft. (about 0.6 meters) for the expansion section 60, 30 ft. (about 9meters) for the first cooling section 62, and 50 ft. (about 15 meters)for the second cooling section 66.

The expansion section 60 must be of relatively short length which,however, is sufficient to allow for a gradual expansion of the sleeve10. The angle formed by the axis of the pipe 56, 60 and an extension ofthe wall of the frusto-conical pipe 60 (defined as the conical angle ofexpansion) is less than 60° and preferably less than 30° but greaterthan 10°.

As mentioned earlier an induction heating device 40 is located betweenthe metering supply 12, 38 of the sleeve 10 and the heating section 56,60 of pipe. This induction heating device 40, which is used for rapidlyincreasing the temperature at the inside of the sleeve, can, however, bean integral part of the heating pipe 56, 60. In this case, the sectionon which the induction coil is mounted is fabricated from an insulatingmaterial. It is desirable that this pipe not restrict to any significantdegree the passage of electromagnetic energy to the inner metallic core46 (FIG. 2) of the sleeve 10. When the heating device 40 is installed asan integral part of the heating pipe 56, 60, its location can be anypoint between the upstream end of the pipe 56 and the expansion section60.

As mentioned earlier a lubricant sealing box 42 is located at theentrance to the heating pipe 56. The purpose of this lubricant sealingbox 42 is to collect any lubricant which may leak out of the heatingpipe by improper sealing of the elastomeric seal over the sleeve 10being fed into the heating pipe. Such leaks may be due, for example, tolack of roundness of the sleeve. The sealing box 42 may be of aconstruction similar to that used for water seals in extrusion lines.This box 42 is connected to the lubricant supply system.

Also, as indicated earlier, at the end of the expansion pipe 60, a firstsection 62 of the cooling pipe 58 is installed. This cooling pipe 58 hasas its upstream end an interior diameter equal to the downstream endinterior diameter of the expansion pipe 60. This diameter can beconstant or it can become gradually smaller with the shrinkage of theexpanded sleeve in the first cooling section 62. The length of thissection 62 of the cooling pipe ensures that the outer part of theexpanded sleeve 10 has reached a hard condition before passing to thepressurized cooling section 66. The length of this section 62 ispreferably such that no further increase in diameter of the sleeve 10will take place while passing through the subsequent cooling section 66.The lubricant sealing section 72 is located at the end of the section 62of the cooling pipe. The cooling mantle 66 is connected to the coolingliquid supply system 80, 82, 84 which allows removal of the heatingenergy from the expanded sleeve without causing deformation or internalshrinkage voids.

The high pressure water cooling section 66 of the cooling pipe 58 has aconstruction similar to that used in the cooling of power cables andenables the application of a controlled maximum fluid pressure to theoutside of the expanded sleeve 10 which is about the same as the fluidpressure applied to the inside of the sleeve. The optimal length of thissection 66 of the cooling pipe 58 is determined in accordance with theheat energy remaining in the sleeve and the speed at which the operationis executed. When the expanded sleeve leaves the cooling pipe, atemperature not greater than about 40° C. exists at the hottest point inthe core. The direct contact between the cooling water and the expandedsleeve 10 provides for efficient heat transfer.

At the downstream end of the cooling pipe 66 a water seal 76 isprovided. This water seal is incorporated into a water seal box 78followed by a water dryer 86. After passing through this structure theexpanded sleeve passes through a pull-out capstan 88 and is wound onto atake-up reel 90. The internal pressure in the sleeve 10 is maintainedthroughout the operation, minimizing in this manner the formation ofdefects such as voids, cracks, etc. The stranded core 46 (FIG, 2) easilyallows passage of the pressurizing fluid throughout the interior of thesleeve 10 from one end to the other. The pull-out capstan 88 is of sucha nature as to minimize the deformation of the sleeve 10. Caterpillarpull-out capstans, as illustrated, are most suitable for this purpose.

At the completion of the sleeve manufacture, the metallic core 46 (FIG.2) can be pulled out of the sleeve 10. The hardened, crosslinked sleeve10 will maintain its shape until heated for shrinkage. The sleeve 10 canbe used over any cable having an equivalent diameter larger than theoriginal inside diameter of the sleeve 10. In use the sleeve 10 is cutinto lengths as required by the cable joining operation.

In an alternative method of manufacture of the sleeves, illustrated inFIG. 5, the entire process of extruding the composite insulation systemover a metallic core 46 and the curing, expansion and cooling arecombined into one continuous operation with substantial reduction incosts and time of manufacture. Except for differences described below,the process of FIG. 5 is similar to that described previously in thisdisclosure.

In the case of FIG. 5, the metallic core 46 is supplied from a reel 120,through a metering capstan 122 to a set of three extruders 124, 126,128. Shortly downstream of the metering capstan 122 a device 130 appliesone or more binders (not shown) over the core 46. These binders arepreferably of a high temperature resistant film or paper (not shown).The purpose of these tapes is to smoothen the inner sleeve surface. Thetape is removed from the sleeve 10 together with the metallic core,before the sleeve is used in joining or splicing cables. The tape ispreferably of a porous nature, such as cellulose or synthetic paper.

Upstream of the first extruder crosshead 124 a core pressurizing system134 with a fluid entrance 136 and a seal 37 makes it possible tomaintain internal fluid pressure in the hollow or stranded metal core46. A pipe 137a surrounds the core 46, and the fluid introduced into thepipe from source 138 penetrates the tape applied by the device 130 andpressurizes the interior of the core 46. In the case where the extrudersare arranged in tandem, the pressurization means 138 such as a tank orcompressor supplies dry air or nitrogen to the outside of the layerextruded by the extruder 124 at a point 140 between the extrusion head124 and the heads 126, 128. This pressure is regulated to be slightlyhigher than the pressure applied to the inner core and prevents blowoutof the layer applied by the extruder 124. The pressure applied at 140 iscontained within a pipe 141.

After the sleeve 10 leaves the last section of the extruder head inwhich the outer insulation shield is applied, it enters into a heatingor curing pipe 142 having an interior diameter somewhat larger than thatof the die of the downstream extruder 128. The inner diameter of thispipe 142 is calculated to allow for expansion during the crosslinkingprocess which takes place while the sleeve 10 passes through the curingpipe. Heating means such as an AC power source 142a similar to the ACpower source 112 (FIG. 3) is provided. The sleeve 10 is lubricated fromits outside by means of a lubricating system 144 which feeds a lubricantliquid having a molecular weight high enough to provide molecules of asize incapable of penetrating into the semiconducting layer. The lengthof the curing pipe 142 is selected so that, when the insulating systemreaches the end of the curing pipe, it has been fully crosslinked(cured). The pipe 142 may have to be longer than the previouslydescribed heating pipe 56, 60 or the speed of the process may have to bereduced.

In the process of FIG. 5 also, the cooling pipe 62 may have to be largerbecause higher temperatures than in the previous process may be used. Inboth processes, the cooling of the expanded sleeve is gradual. In thefirst cooling section 62, the sleeve 10 is hardened to the point that nofurther deformation thereof occurs when the sleeve comes into directcontact with the cooling medium of the second section 66 (FIG. 3). Inthe case of very thick sleeves, the temperature of the pressurizationmeans in the second cooling pipe 66 may be reduced gradually from thepoint of sleeve entrance to the point of exit. The cooling means ispressurized at a pressure no greater than the pressure maintained insidethe sleeve.

In FIG. 5, the application of the internal pressure is provided by thesupply 138 of fluid (gas or liquid) through an entrance 136 locatedupstream of the first extrusion head 124. In order to minimize the lossof pressure the conductor 46 (FIG. 2) is supplied through theclose-tolerance cylindrical pipe 137a, and, at the upstream end of thispipe, the seal 137 is provided.

Internal pressure is applied through the entrance 136 only after theinitial curing of the sleeve 10 has been achieved and pre-selecteddimensions are checked at the exit of the curing pipe (between curingand expansion pipes). This can be facilitated by providing one or moretransparent portions or windows (not shown) at appropriate locations inthe piping system. Before applying the internal pressure, the startingor leading end of the sleeve 10 is sealed to allow for maintaining withrelative ease the internal expansion pressure. During subsequent usage,the sleeve may be shrunk back to an outside diameter equivalent to theinside diameter of the curing pipe 142. Immediately following theapplication of the internal pressure, the part of the continuous sleevepassing through the expansion section 143 of the curing pipe tends toattain the maximum diameter of this pipe section 143.

The above described process for the manufacture of shrinkable sleevesensures a high consistency in quality by providing sleeves manufacturedunder very high curing and cooling pressures. This process also allowsfor the manufacture of joining sleeves for very high voltage cableshaving considerable wall thickness, which otherwise would be difficultand time consuming to manufacture. The high pressure utilized duringboth curing and cooling ensures the elimination of voids and microvoidsin the insulation body.

Installation of the shrinkable joints in the field, as explained in saidcopending U.S. patent application Ser. No. 319,429, takes place afterpreparation of the cable for joining. First a resilient stress gradedmaterial is applied over the exposed cable insulation, and over thisresilient stress graded layer the three-layer composite sleeve 10 isshrunk. Furthermore, a grease-like material is utilized for sealing thecable ends, to make them resistant to the penetration and longitudinalflow of moisture, which otherwise might work its way from the interfacebetween the resilient stress graded material and the insulation into themass of the insulation.

It has been found that commercially available resilient stress gradedmaterials may affect the integrity of the high resistive semiconductinglayer of the composite sleeve, by migration of liquid dielectrics suchas oils or plasticizers utilized in the manufacture of the stress gradedmaterial. It has also been found that an alternative, novel stressgraded compound overcomes this problem and at the same time constitutesa moisture seal that prevents penetration in the longitudinal directionalong the interface of the newly developed compound and the adjacentextruded materials.

This newly developed composite is made of a dimethyl silicone liquid andsilicone carbide powder having a particle size capable of passingthrough a 400 mesh screen. The two are mixed in a volumetric proportionof powder to 1 part liquid which is within the range of 0.5 part to 2.0parts. Preferably, the ratio is 1 part of powder to 1 part of liquid byvolume. In addition, fumed silica such as Cabosil by Cabot Corporationmay be added to minimize the flow of this compound when heated toelevated temperature or when a low viscosity mixture is obtained becauseof the use of lower viscosity fluids.

In the manufacture of one version of the described stress gradedmaterial where fumed silica is not used, the silicone fluid is firstbrought to elevated temperature and subjected to an evacuation to removeany gas entrapped. Subsequently, the silicone carbide is added in acontinuous mixing procedure during which an intimate contact between thetwo materials is obtained. The mixing, in a gas-free environment, avoidsor minimizes the presence of voids in this composite material andimproves the characteristics of the stress graded material. Mixing in anair environment, without evacuation, is also feasible. In this casefumed silica may be added. This process, however, requires the use ofheavier thicknesses of the stress graded material to avoid the weaknessintroduced by voids or microvoids in its mass.

The application of these resilient compounds in the preparation of cablejoints requires extruding a thin layer of compound, typically 20 to 30mils thick, and applying this layer between two sheaths of disposablefilm, one of them to be removed just prior to application of thecompound over the cable and the second one to be removed just prior toshrinking the composite sleeve over the joint. The characteristics ofthese disposable layers are such that they do not adhere permanently tothe surface of the compound.

Because of their large molecular weight the dimethyl silicone fluids donot penetrate into the polymeric structure of the semiconductingresistive layer of the composite sleeve 10, and consequently they do notaffect the original resistive characteristics of this layer. Because ofthis property, in addition to its moisture resistant characteristics andits resilience, so as to conform to any crevices in the polymericinterfaces and accommodate the dimensional changes occurring in theadjacent material during heating and cooling of the joint, it is wellsuited to the manufacture of power cable joints. It has also been foundthat the stress graded characteristics of the new mixture are as good asor better than those of other stress graded materials now available inthe market.

Several tests have confirmed the advantages of using this new stressgraded compound. Longitudinal dielectric strength tests performed withthe new compound in a version made without fumed silica, applied a 5"long layer between two concentric layers of insulation. The voltage wasincreased 10% every 5 minutes. Breakdown occurred in one test at 95 kVand in another test at 100 kV. These values compare favorably with about80 to 90 kV breakdowns obtained for commercially available stress gradedmaterial, tested under similar conditions. It has also been found thatjoints submerged in water with accelerating voltage aging conditionsapplied to them, without having any protection whatsoever to stop theflow of water into the area where the stress graded material is applied,are not affected by the presence of the water. This test has beenconducted for three continuous months. In addition, tests have beenconducted to establish whether the new compound will flow under hightemperature conditions. No flow has been detected in spite of keepingthe experimental joints in a vertical position cycling to 130° C. for 30days.

It should be noted that the expansion process for sleeves described inthis disclosure is also very suitable for the manufacture of cables withextruded insulation for use at cryogenic temperatures where it becomes arequirement, due to the dissimilar coefficients of contraction of themetal core and of the dielectric system, that extra radial space beprovided between the interfaces of the metal and the insulation toprevent cracking of the insulation.

Thus there is provided in accordance with the invention a novel andhighly effective method of and apparatus for manufacturing long lengthsof a heat-shrinkable sleeve for use in splicing electrical cables andthe like, and a novel and highly effective stress-graded compound to beused in such splicing. Many modifications of the preferred embodimentsof the invention disclosed herein will readily occur to those skilled inthe art upon considering this disclosure, and all such modifications areintended to be covered by the appended claims.

What is claimed is:
 1. Apparatus for manufacturing long lengths of aheat-shrinkable sleeve for use in splicing electrical cables and thelike, comprisingforming means for forming an elongated sleeve having aplurality of layers formed of a thermosettable material around anelongated core; means for continuously advancing said core and saidsleeve in a generally axial direction; heating pipe means cooperatingwith said core and sleeve for surrounding, heating, and curing a portionof said sleeve, said heating pipe means being formed with an expansionsection of progressively increasing interior diameter, means forintroducing a fluid under pressure into the core, thereby internallypressurizing the sleeve against said heating pipe means to effect aradial expansion of the heated, cured portion thereof within saidexpansion section, and cooling means cooperating with said core andsleeve for cooling the expanded sleeve to stabilize it.
 2. Apparatusaccording to claim 1 wherein said core is made of a magnetizablematerial, further comprising induction heating means cooperatingtherewith for heating said core, thereby heating said sleeve frominside.
 3. Apparatus according to claim 1 further comprising lubricatingmeans for introducing a lubricant between said heating pipe means andsaid sleeve for facilitating passage of said sleeve through said heatingpipe means.
 4. Apparatus according to claim 3 further comprising annularsealing means surrounding and cooperating with said sleeve to facilitatepassage therethrough of said sleeve and retard leakage therethrough ofsaid lubricant.
 5. Apparatus according to claim 1 further comprisingmeans for supplying a cooling fluid to said cooling means to regulatesaid cooling and stabilizing of said expanded sleeve.
 6. Apparatusaccording to claim 5 further comprising annular sealing meanssurrounding and cooperating with said sleeve to facilitate passagetherethrough of said sleeve and retard leakage therethrough of saidcooling fluid.
 7. Apparatus according to claim 1 wherein said formingmeans comprises means for extruding said sleeve around said core. 8.Apparatus according to claim 7 wherein said extrusion means comprises aplurality of extrusion devices spaced apart longitudinally with respectto the direction of movement of said core and sleeve.
 9. Apparatusaccording to claim 8 further comprising means for supplying a fluidunder pressure to the exterior of said extruded sleeve to preventblowout thereof by said pressurized fluid introduced into said core.